WO2013161975A1 - Composition de résine et son utilisation - Google Patents

Composition de résine et son utilisation Download PDF

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WO2013161975A1
WO2013161975A1 PCT/JP2013/062325 JP2013062325W WO2013161975A1 WO 2013161975 A1 WO2013161975 A1 WO 2013161975A1 JP 2013062325 W JP2013062325 W JP 2013062325W WO 2013161975 A1 WO2013161975 A1 WO 2013161975A1
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group
resin composition
fluororesin
resin
polar functional
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PCT/JP2013/062325
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English (en)
Japanese (ja)
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渋谷　光夫
章誠 稲熊
泰広 平野
前田　誠二
西　栄一
茂 相田
晋太郎 福永
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日本合成化学工業株式会社
旭硝子株式会社
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Application filed by 日本合成化学工業株式会社, 旭硝子株式会社 filed Critical 日本合成化学工業株式会社
Priority to US14/379,530 priority Critical patent/US9487650B2/en
Priority to CN201380021321.3A priority patent/CN104245829B/zh
Priority to EP13781259.0A priority patent/EP2842998B1/fr
Publication of WO2013161975A1 publication Critical patent/WO2013161975A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L29/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
    • C08L29/02—Homopolymers or copolymers of unsaturated alcohols
    • C08L29/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F216/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
    • C08F216/02—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an alcohol radical
    • C08F216/04—Acyclic compounds
    • C08F216/06—Polyvinyl alcohol ; Vinyl alcohol
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F218/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid or of a haloformic acid
    • C08F218/02—Esters of monocarboxylic acids
    • C08F218/04—Vinyl esters
    • C08F218/08—Vinyl acetate
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00—Chemical modification by after-treatment
    • C08F8/12—Hydrolysis
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/005—Processes for mixing polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08L27/18—Homopolymers or copolymers or tetrafluoroethene
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/621—Binders
    • H01M4/622—Binders being polymers
    • H01M4/623—Binders being polymers fluorinated polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2800/00—Copolymer characterised by the proportions of the comonomers expressed
    • C08F2800/20—Copolymer characterised by the proportions of the comonomers expressed as weight or mass percentages
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2329/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
    • C08J2329/02—Homopolymers or copolymers of unsaturated alcohols
    • C08J2329/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2427/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2427/22—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers modified by chemical after-treatment
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00—Properties
    • C08L2201/14—Gas barrier composition
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00—Applications
    • C08L2203/16—Applications used for films
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Definitions

  • the present invention is a resin composition containing a polyvinyl alcohol-based resin, more specifically, a resin composition having excellent gas barrier properties and bending fatigue resistance, excellent solvent resistance, and low surface free energy, and It is related with the use of a composition, and the manufacturing method of the said composition.
  • PVA resins are suitable as packaging materials and binders for various articles because they are excellent in gas barrier properties, toughness, transparency, solvent resistance, and the like.
  • the PVA resin usually has a melting point and a decomposition temperature close to each other, melt molding is substantially impossible.
  • a molding method of PVA-based resin it is necessary to adopt a method of forming an aqueous solution and then casting and drying it to form a film, or applying and drying on the surface of various base materials.
  • this has been a major obstacle to the widespread use of PVA-based resins for packaging materials.
  • side-chain 1,2-diol-containing PVA resin PVA resins having a 1,2-diol structural unit in the side chain
  • side-chain 1,2-diol-containing PVA resin has lower crystallinity and lower melting point than conventional PVA resins due to steric hindrance of the side chain. Nevertheless, it has a gas barrier property comparable to that of conventional PVA-based resins.
  • the side chain 1,2-diol-containing PVA resin exhibits excellent gas barrier properties even when the crystallinity is lower than that of conventional PVA resins due to strong hydrogen bonding due to side chain hydroxyl groups in the amorphous part. It is guessed.
  • the high molecular chain crystallinity and the strength of the binding force due to hydrogen bonds in PVA-based resins can exhibit excellent gas barrier properties, but they are more flexible and impact resistant than other thermoplastic resins. Cause inferiority.
  • Patent Document 2 discloses a block copolymer having two or more polymer blocks made of a vinyl aromatic compound and one or more polymer blocks made of a conjugated diene compound as a thermoplastic elastomer. It is disclosed that flexibility and impact resistance are improved by blending a hydrogenated block copolymer obtained by hydrogenation of PVA with a PVA resin.
  • the present inventors have further studied for the purpose of a PVA-based resin composition having improved bending fatigue resistance in a resin composition using a side-chain 1,2-diol-containing PVA-based resin.
  • a resin composition is proposed in which a mixture of a block copolymer having no carboxyl group and a block copolymer having a carboxyl group is blended (Japanese Patent Application No. 2011-74364 (Patent Document 3)).
  • the PVA resin composition disclosed in Patent Document 3 can be melt-molded, has improved bending fatigue resistance, and retains the gas barrier properties inherent to PVA resins.
  • the block copolymer which is an elastomer component due to the block copolymer which is an elastomer component, there is a new problem that the excellent solvent resistance inherent in the PVA resin is impaired.
  • the decrease in solvent resistance limits the use of the resin composition as a packaging container, various binders, and adhesives.
  • the present invention has been made in view of the circumstances as described above, and the object thereof is a resin composition containing a PVA resin that can be melt-molded, and has an inherent gas barrier property,
  • An object of the present invention is to provide a resin composition having improved flexibility such as bending fatigue resistance without impairing solvent resistance, and use thereof.
  • the resin composition of the present invention includes a polyvinyl alcohol resin (A) containing a structural unit represented by the following formula (1), and a fluorine having a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond Resin (B) (hereinafter referred to as “polar functional group-containing fluororesin (B)”).
  • A polyvinyl alcohol resin
  • B fluorine having a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond Resin
  • B polar functional group-containing fluororesin
  • the polar functional group is preferably a carbonyl-containing group or a hydroxyl group
  • the carbonyl-containing group includes a carbonate group, a haloformyl group, an aldehyde group, a ketone group, a carboxyl group, an alkoxycarbonyl group, a carboxylic acid anhydride group, and an isocyanato group. It is preferably at least one selected from the group consisting of groups.
  • the polar functional group-containing fluororesin (B) is preferably a copolymer containing at least tetrafluoroethylene as a constituent monomer, and further preferably contains ethylene as a constituent monomer.
  • the melting point of the polar functional group-containing fluororesin (B) is preferably 120 to 220 ° C.
  • the content mass ratio (A / B) between the polyvinyl alcohol resin (A) and the polar functional group-containing fluororesin (B) is preferably 98/2 to 2/98.
  • the method for producing a resin composition of the present invention has a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond with a polyvinyl alcohol resin (A) containing the structural unit represented by the above formula (1).
  • the present invention also includes pellets of resin compositions and emulsified dispersions as uses of the resin composition of the present invention. Further applications include melt-formed products and binders.
  • the resin composition of the present invention contains a melt-moldable PVA resin (A), and further contains a fluororesin (B) having a polar functional group capable of reacting with the PVA resin or forming a hydrogen bond. Therefore, it has flexibility such as bending fatigue resistance without impairing the inherent gas barrier properties and solvent resistance of the PVA resin.
  • FIG. It is the microscope picture (5000 times) which imaged the mode of the film after the solvent resistance test of Example 2.
  • FIG. It is the microscope picture (5000 times) which imaged the mode of the film after the solvent-proof test of the comparative example 1.
  • 4 is a voltammogram obtained in the electrochemical stability test of Example 4.
  • 4 is a voltammogram obtained in the electrochemical stability test of Comparative Example 2.
  • 4 is a voltammogram obtained in the electrochemical stability test of Comparative Example 3.
  • the description of the constituent requirements described below is an example (representative example) of an embodiment of the present invention, and is not limited to these contents.
  • the resin composition of the present invention has (A) a polyvinyl alcohol resin having a 1,2-diol structural unit in the side chain (side chain 1,2-diol-containing PVA resin), and (B) a polar functional group. It is a resin composition containing a fluororesin (polar functional group-containing fluororesin).
  • a fluororesin polar functional group-containing fluororesin
  • the side chain 1,2-diol-containing PVA resin used in the present invention refers to a polyvinyl alcohol resin having a side chain 1,2-diol unit represented by the following formula (1).
  • R 1 to R 6 each independently represents a hydrogen atom or an organic group.
  • R 1 to R 6 are preferably all hydrogen atoms, but may be organic groups as long as the resin properties are not significantly impaired.
  • the organic group is not particularly limited, but is preferably an alkyl group having 1 to 4 carbon atoms such as a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group, an isobutyl group, or a tert-butyl group. You may have substituents, such as a halogen group, a hydroxyl group, an ester group, a carboxylic acid group, and a sulfonic acid group, as needed.
  • X is a single bond or a bonded chain, and is preferably a single bond from the viewpoint of improving crystallinity and reducing free volume (intermolecular void) in an amorphous part.
  • the bonding chain is not particularly limited, but other hydrocarbons such as alkylene, alkenylene, alkynylene, phenylene, naphthylene (these hydrocarbons may be substituted with halogen such as fluorine, chlorine, bromine, etc.) , —O—, — (CH 2 O) m—, — (OCH 2 ) m—, — (CH 2 O) mCH 2 —, —CO—, —COCO—, —CO (CH 2 ) mCO—, — CO (C 6 H 4 ) CO—, —S—, —CS—, —SO—, —SO 2 —, —NR—, —CONR—, —NRCO—, —CSNR—, —NR
  • R is an optional substituent each independently, a hydrogen atom, an alkyl group are preferred, and m is a natural number
  • alkylene having 6 or less carbon atoms, particularly methylene, or —CH 2 OCH 2 — is preferable from the viewpoint of viscosity stability during production, heat resistance, and the like.
  • R 1 to R 6 are all hydrogen atoms, and X is a single bond. That is, the structural unit represented by the following structural formula (1a) is most preferable.
  • the side chain 1,2-diol-containing PVA resin having the above-described structure is obtained by reacting a side chain 1,2-diol unit, that is, a side chain OH group with a polar functional group of the B component, or hydrogen. It becomes possible to connect with each other by the combination. Thereby, the affinity of A component and B component improves. The affinity of both components is improved by adding a polar functional group-containing fluororesin (or side chain) as the B component in the side chain 1,2-diol-containing PVA resin (or polar functional group-containing fluororesin) as the matrix component. 1,2-diol-containing PVA resin).
  • the conventional PVA resin having no 1,2-diol unit in the side chain also has an OH group in the molecular chain, but all the OH groups in the main chain are secondary hydroxyl groups. For this reason, compared with the primary hydroxyl group in the 1,2-diol unit in the side chain, the reactivity with the polar functional group contained in the component B is small, and it is difficult to obtain a uniformly dispersed resin composition. .
  • Such a side chain 1,2-diol-containing PVA resin is not particularly limited, but (i) a method of saponifying a copolymer of a vinyl ester monomer and a compound represented by the following formula (2), ii) a method of saponifying and decarboxylating a copolymer of a vinyl ester monomer and a vinyl ethylene carbonate represented by the following formula (3), (iii) a vinyl ester monomer and 2,
  • the copolymer with 2-dialkyl-4-vinyl-1,3-dioxolane can be produced by a method of saponification and deketalization.
  • R 1 to R 6 are all the same as in the formula (1).
  • R 7 and R 8 are each independently hydrogen or R 9 —CO— (wherein R 9 is an alkyl group having 1 to 4 carbon atoms).
  • R 10 and R 11 are each independently a hydrogen atom or an organic group.
  • the methods (i), (ii), and (iii) for example, the method described in JP-A-2006-95825 can be employed.
  • the method (i) is preferable in that it is excellent in copolymerization reactivity and industrial handling, and in particular, R 1 to R 6 are hydrogen, X is a single bond, R 7 and R 8 are R 9 —CO—. 3,4-diasiloxy-1-butene in which R 9 is an alkyl group is preferred, and among these, 3,4-diacetoxy-1-butene in which R 9 is a methyl group is particularly preferred.
  • vinyl ester monomers examples include vinyl formate, vinyl acetate, vinyl propionate, vinyl valelate, vinyl butyrate, vinyl isobutyrate, vinyl pivalate, vinyl caprate, vinyl laurate, vinyl stearate, vinyl benzoate, versatic.
  • vinyl acid acid etc. are mentioned, vinyl acetate is preferably used especially from an economical viewpoint.
  • ⁇ -olefins such as ethylene and propylene; hydroxy group-containing ⁇ -olefins such as 3-buten-1-ol and 4-penten-1-ol; and vinylene carbonates and acrylic acid
  • ⁇ -olefins such as ethylene and propylene
  • hydroxy group-containing ⁇ -olefins such as 3-buten-1-ol and 4-penten-1-ol
  • vinylene carbonates and acrylic acid Unsaturated acids or salts thereof, mono- or dialkyl esters, nitriles such as acrylonitrile, amides such as methacrylamide, olefin sulfonic acids such as ethylene sulfonic acid, allyl sulfonic acid, methallyl sulfonic acid or salts thereof It may be copolymerized.
  • ethylene that forms a eutectic with a vinyl alcohol structural unit is particularly preferable.
  • the polymerization of the vinyl ester monomer and the above formula (2), (3), or (4) can be carried out by any known polymerization method such as solution polymerization, suspension polymerization, emulsion polymerization and the like. Among them, it is preferable to carry out solution polymerization under reflux that can efficiently remove reaction heat.
  • solvent for the solution polymerization alcohol is usually used, and preferably a lower alcohol having 1 to 3 carbon atoms is used.
  • a known saponification method that has been conventionally performed with a PVA resin can be employed. That is, it can be carried out using an alkali catalyst or an acid catalyst in a state where the copolymer is dissolved in alcohol or water / alcohol solvent.
  • the alkali catalyst include alkali metal hydroxides and alcoholates such as potassium hydroxide, sodium hydroxide, sodium methylate, sodium ethylate, potassium methylate, and lithium methylate.
  • the reaction temperature of the saponification reaction is preferably 20 ° C to 60 ° C. If the reaction temperature is too low, the reaction rate decreases and the reaction efficiency decreases, and if it is too high, the reaction solvent may have a boiling point or higher, and the safety in production is reduced.
  • saponification is performed under high pressure using a tower type continuous saponification tower having high pressure resistance, it is possible to saponify at a higher temperature, for example, 80 to 150 ° C., and a small amount of saponification catalyst. It is also possible to obtain a high saponification degree for a short time.
  • the degree of polymerization in the side chain 1,2-diol-containing PVA resin as described above is usually 250 to 1000, preferably 300 to 700, more preferably 400 to 600. If the degree of polymerization becomes too high, the melt viscosity becomes too high, and a load is applied to the extruder at the time of melt kneading, and there is a possibility that the resin temperature becomes high due to shear heat generation at the time of melt kneading and the resin is deteriorated. On the other hand, if the degree of polymerization is too low, the molded product becomes brittle, so that cracks tend to occur and the gas barrier property tends to decrease.
  • the degree of saponification of the vinyl ester moiety in the side chain 1,2-diol-containing PVA resin is a value measured based on JIS K6726, and is usually 98 to 100 mol%, preferably 99 to 100 mol%, more preferably Is 99.5 to 99.9 mol%. If the degree of saponification is too low, it means that the content of OH groups decreases, and the gas barrier property tends to be lowered. On the other hand, a highly saponified and completely saponified PVA resin tends to be difficult to produce industrially.
  • the content of the structural unit represented by the above formula (1) is usually 2 to 20 mol%, preferably 4 to 15 mol%, based on the whole PVA resin constituting monomer. More preferably, it is 5 to 12 mol%.
  • the side chain 1,2-diol content increases, the melting point and crystallization degree decrease, which is preferable in terms of improving melt moldability during extrusion, but tends to decrease the productivity of the PVA resin. There is.
  • the content of the side chain 1,2-diol is too low, it will be close to the unmodified PVA resin, making melt molding difficult.
  • since there are few reaction points or hydrogen bond formation parts with the polar functional group containing fluororesin which is B component it exists in the tendency for the dispersibility of B component in a resin composition to fall.
  • the polar functional group-containing fluororesin used in the present invention refers to a fluoropolymer in which a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond is introduced into the fluororesin.
  • the polar functional group is a functional group capable of reacting with a hydroxyl group or a functional group capable of forming a hydrogen bond, preferably a carbonyl-containing group or a hydroxyl group, more preferably a carbonyl-containing group.
  • the carbonyl-containing group is at least one selected from the group consisting of carbonate groups, haloformyl groups, aldehyde groups (including formyl groups), ketone groups, carboxyl groups, alkoxycarbonyl groups, carboxylic anhydride groups, and isocyanato groups. It is preferably a seed, more preferably a carbonate group, a fluoroformyl group, a carboxyl group, a methoxycarbonyl group, an ethoxycarbonyl group, or a carboxylic acid anhydride group, and most preferably a carboxylic acid anhydride group.
  • the fluororesin constituting the polar functional group-containing fluororesin is preferably a fluorocopolymer containing at least tetrafluoroethylene as a constituent monomer.
  • the fluorine-based copolymer includes hexafluoropropylene, vinylidene fluoride, perfluoro (alkyl vinyl ether), CH 2 ⁇ CX (CF 2 ) n Y (X and Y are each independently a fluorine atom or a hydrogen atom, n Is an olefinic vinyl monomer such as ethylene and propylene, vinyl ethers and vinyl esters, in addition to other fluorine-containing vinyl monomers such as monomers represented by the formula (hereinafter referred to as “FAE”) Other halogen-containing vinyl monomers may be copolymerized.
  • n in the formula is preferably 2 to 8, more preferably 2 to 6, and particularly preferably 2, 4, 6.
  • n is less than 2, the heat resistance and stress crack resistance of the molded article of the resin composition tend to decrease.
  • n exceeds 10 polymerization reactivity may become insufficient.
  • n is in the range of 2 to 8, the polymerization reactivity of FAE is good.
  • it becomes easy to obtain a molded body excellent in heat resistance and stress crack resistance. 1 type (s) or 2 or more types can be used for FAE.
  • FAE Preferable specific examples of such FAE include CH 2 ⁇ CH (CF 2 ) 2 F, CH 2 ⁇ CH (CF 2 ) 4 F, CH 2 ⁇ CH (CF 2 ) 6 F, CH 2 ⁇ CF (CF 2) 3 H and the like.
  • CH 2 ⁇ CH—Rf Rf is a C 2-6 perfluoroalkyl group
  • fluororesin examples include tetrafluoroethylene / perfluoro (alkyl vinyl ether) copolymer, tetrafluoroethylene / hexafluoropropylene copolymer, tetrafluoroethylene / perfluoro (alkyl vinyl ether) / hexafluoropropylene copolymer.
  • An alkyl group) type copolymer is preferably selected from the group consisting of copolymers.
  • an ethylene / tetrafluoroethylene / hexafluoropropylene copolymer an ethylene / tetrafluoroethylene copolymer (hereinafter, “E” for ethylene, “TFE” for tetrafluoroethylene, and “HFP” for hexafluoropropylene)
  • E ethylene
  • TFE tetrafluoroethylene
  • HFP hexafluoropropylene
  • Ethylene / tetrafluoroethylene may be referred to as an E / TFE copolymer
  • ethylene / tetrafluoroethylene / hexafluoropropylene copolymer may be referred to as an “E / TFE / HFP copolymer”.
  • the E / TFE copolymer or the E / TFE / HFP copolymer is added with CH 2 ⁇ CH—Rf ( It is also preferable to copolymerize a comonomer in which Rf represents a C 2-6 perfluoroalkyl group. Note that the number of carbon atoms in Rf in the CH 2 ⁇ CH—Rf is most preferably 4.
  • a fluororesin As a method for introducing a polar functional group into the fluororesin as described above, when a fluororesin is produced by polymerizing a fluorine-containing vinyl monomer such as TFE or HFP, a vinyl having a fluorofunctional vinyl monomer and a polar functional group is used.
  • a fluorine-containing vinyl monomer such as TFE or HFP
  • a method of copolymerizing with a monomer a method of introducing a polar functional group into a polymer terminal by polymerizing a fluorine-containing vinyl monomer in the presence of a polymerization initiator having a polar functional group or a chain transfer agent; A method of kneading a vinyl monomer and a fluororesin having radiation, and then irradiating with radiation; kneading a vinyl monomer having a polar functional group, a fluororesin and a radical initiator, and then melt-extruding to have the polar functional group Examples thereof include a method of graft polymerization of a comonomer onto a fluororesin.
  • vinyl monomer having a polar functional group examples include maleic anhydride, itaconic anhydride, citraconic anhydride, 5-norbornene-2,3-dicarboxylic anhydride (bicyclo [2.2.1] hept-2-ene Monomers giving carboxylic anhydride groups such as -5,6-dicarboxylic anhydride; acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, citraconic acid, crotonic acid, bicyclo [2.2.
  • a peroxide having a peroxycarbonate group or a peroxide having a peroxyester can be used, and among them, a peroxide having a peroxycarbonate group is more preferably used.
  • the peroxide having a peroxycarbonate group include diisopropyl peroxycarbonate, di-n-propyl peroxydicarbonate, t-butyl peroxyisopropyl carbonate, bis (4-t-butylcyclohexyl) peroxydicarbonate, di-2 -Ethylhexyl peroxydicarbonate is preferably used.
  • chain transfer agent having a polar functional group examples include alcohols such as methanol, ethanol, propanol, and butanol, carboxylic acids such as acetic anhydride, thioglycolic acid, and thioglycol.
  • the content of polar functional groups in component B is preferably 0.01 to 10 mol%, more Preferably it is 0.05 to 5 mol%, most preferably 0.1 to 3 mol%.
  • amount of the functional group is too small, the affinity with the A component is too low, and it becomes difficult to achieve fine dispersion of the B component, and as a result, it becomes difficult to obtain a homogeneous resin composition.
  • the polar functional group-containing fluororesin used in the present invention preferably has a melting point of 120 to 220 ° C, more preferably 150 to 210 ° C, and still more preferably 170 to 190 ° C. If the melting point of the component A, which is the main component of the resin composition, is too high, it is necessary to increase the melting temperature to 250 to 290 ° C. when producing the composition. It causes color deterioration and is not preferable. Usually, in the polar functional group-containing fluororesin having a polar functional group content in the above range, the melting point is in the above range.
  • the volume flow rate (hereinafter referred to as “Q value”) of the fluororesin used for the component (B) is 0.1 to 1000 mm 3 / sec, preferably 1 to 500 mm 3 / sec, more preferably 2 to 200 mm. 3 / sec.
  • the Q value is an index representing the melt fluidity of a resin that becomes a problem when a fluororesin is melt-molded, and is a measure of the molecular weight. That is, a large Q value indicates a low molecular weight, and a small Q value indicates a high molecular weight.
  • the Q value is a resin when extruded into an orifice having a diameter of 2.1 mm and a length of 8 mm under a load of 7 kg at a temperature 50 ° C. higher than the melting point of the fluororesin using a flow tester manufactured by Shimadzu Corporation. Extrusion speed of If the Q value is too small, extrusion molding of the fluororesin becomes difficult, and if it is too large, the mechanical strength of the resin decreases.
  • the radical polymerization initiator generally charged by charging a fluorine-containing vinyl monomer and other comonomers into a reactor is used.
  • a method of copolymerization using a chain transfer agent can be employed.
  • polymerization methods include bulk polymerization, solution polymerization using organic solvents such as fluorinated hydrocarbons, chlorinated hydrocarbons, fluorinated chlorohydrocarbons, alcohols and hydrocarbons as polymerization media; Suspension polymerization using an aqueous medium and, if necessary, an appropriate organic solvent; emulsion polymerization using an aqueous medium and an emulsifier as the polymerization medium may be mentioned, with solution polymerization being most preferred.
  • the polymerization can be carried out as a batch operation or a continuous operation using a one-tank or multi-tank stirring polymerization apparatus, a tube polymerization apparatus, or the like.
  • an initiator having a half-life of 10 hours and a temperature of 0 to 100 ° C. is preferable, and an initiator having a temperature of 20 to 90 ° C. is more preferable.
  • azo compounds such as azobisisobutyronitrile; peroxydicarbonates such as diisopropylperoxydicarbonate; peroxyesters such as tert-butylperoxypivalate, tert-butylperoxyisobutyrate, tert-butylperoxyacetate;
  • Non-fluorinated diacyl peroxides such as ril peroxide, octanoyl peroxide, benzoyl peroxide, lauroyl peroxide; (Z (CF 2 ) p COO) 2 (where Z is a hydrogen atom, a fluorine atom or a chlorine atom, and p is 1
  • a fluorine-containing diacyl peroxide such as potassium persulfate
  • Examples of the polymerization medium include organic solvents such as fluorinated hydrocarbons, chlorinated hydrocarbons, fluorinated chlorinated hydrocarbons, alcohols and hydrocarbons, and aqueous media as described above.
  • Chain transfer agents include alcohols such as methanol and ethanol; chlorofluorohydrocarbons such as 1,3-dichloro-1,1,2,2,3-pentafluoropropane and 1,1-dichloro-1-fluoroethane; Examples thereof include hydrocarbons such as pentane, hexane and cyclohexane; fluorine-containing hydrocarbons such as 1-hydrotridecafluorohexane.
  • the polymerization conditions are not particularly limited.
  • the polymerization temperature is usually preferably 0 to 100 ° C., more preferably 20 to 90 ° C.
  • the polymerization pressure is preferably from 0.1 to 10 MPa, more preferably from 0.5 to 3 MPa.
  • the polymerization time may vary depending on the polymerization temperature and polymerization pressure, but is usually 1 to 30 hours, and more preferably 2 to 10 hours.
  • the resin composition of the present invention includes (A) the side chain 1,2-diol-containing PVA resin, (B) the polar functional group-containing fluororesin, as long as the effects of the present invention are not impaired, if necessary.
  • a conventionally known PVA-based resin having no 1,2-diol unit in the side chain cellulose derivatives such as carboxyethyl cellulose, polymethacrylic acid, polyacrylic acid, etc.
  • Other water-soluble polymers; fluorine resins not containing a polar functional group; other thermoplastic resins such as polyamide, polyester, polyethylene, and polypropylene may be contained.
  • plasticizers such as aliphatic polyhydric alcohols such as ethylene glycol, glycerin and hexanediol; saturated aliphatic amides (eg stearic acid amides), unsaturated fatty acid amides (eg oleic acid amides), bis fatty acid amides (eg Such as ethylene bis-stearic acid amide), low molecular weight polyolefin (for example, low molecular weight polyethylene having a molecular weight of about 500 to 10,000, or low molecular weight polypropylene), anti-blocking agent, antioxidant, coloring agent, antistatic agent, ultraviolet absorber An antibacterial agent; an insoluble inorganic salt (for example, hydrotalcite); a filler (for example, an inorganic filler); an oxygen absorber (for example, a ring-opening polymer of a cycloalkene such as polyoctenylene, or a conjugated diene such as butadiene; Cyclized
  • the resin composition of the present invention comprises the above-mentioned side chain 1,2-diol-containing PVA resin (A), a polar functional group-containing fluororesin (B), and an additive (C) added as necessary. It can be prepared by mixing and mixing quantitatively.
  • the content ratio (A / B) (mass ratio) of (A) side chain 1,2-diol-containing PVA resin and (B) polar functional group-containing fluororesin in the resin composition of the present invention is usually 98/2. To 2/98 is preferable, 98/2 to 30/70 is more preferable, 95/5 to 40/60 is further preferable, and the range of 90/10 to 50/50 is most preferably used. When the content ratio of the component A is too high, the durability, bending fatigue resistance, and stretchability of the molded product are poor and fragile. When the ratio is in the range of 98/2 to 30/70, the side chain 1,2-diol-containing PVA resin (A) forms a matrix of the resin composition, so that the gas barrier property is particularly excellent.
  • / ⁇ B ) is usually from 1/5 to 5/1, particularly preferably from 1/3 to 3/1, more preferably from 1 / 2.5 to 2/1. Even if the melt viscosity ratio is too large or too small, it may not be uniformly mixed during melt kneading. That is, (A) the side chain 1,2-diol-containing PVA resin and (B) the polar functional group-containing fluororesin tend to be closer to each other.
  • the resin composition of the present invention having the above composition is obtained by reacting the side chain 1,2-diol unit of the side chain 1,2-diol-containing PVA resin with the polar functional group of the polar functional group-containing fluororesin. Due to the formation of hydrogen bonds, both components have high affinity, and the polar functional group-containing fluororesin (or the polar functional group-containing fluororesin) in the sea of the side chain 1,2-diol-containing PVA resin (or polar functional group-containing fluororesin) that becomes the matrix Alternatively, the side chain 1,2-diol-containing PVA resin) can be dispersed as fine islands of 1 ⁇ m or less.
  • a molded article such as a film or a coating film, particularly a molded article or coating film of a resin composition in which the PVA resin is used as a matrix, retains the gas barrier property and electrochemical stability inherent to the PVA resin. Furthermore, absorption of external force and stress by the polar functional group-containing fluororesin dispersion layer (domain) and generation of microphrases at the interface between the side chain 1,2-diol-containing PVA resin matrix and the polar functional group-containing fluororesin domain It is considered that the flexibility and the bending fatigue resistance of the PVA resin can be improved by the stress relaxation due to the above. Moreover, since the polar functional group-containing fluororesin has the inherent solvent resistance of the fluororesin, it does not impair the excellent solvent resistance inherent in the PVA resin, so that the resin composition and the molding obtained therefrom The product has excellent solvent resistance.
  • melt kneading method is especially preferable.
  • a melt-kneading apparatus include a kneading machine, an extruder, a mixing roll, a Banbury mixer, a kneader ruder, a blast mill, and the like.
  • a method using an extruder that can be continuously processed and has excellent mixing efficiency Is preferred.
  • twin screw extruder either a single screw extruder or a twin screw extruder can be used.
  • a twin screw extruder particularly a twin screw extruder in which the screw rotation direction is the same, is sufficient by appropriate shearing. This is preferable in that kneading can be obtained.
  • the L / D of the extruder is usually 10 to 80, preferably 15 to 75, more preferably 15 to 70. If L / D is too small, melt-kneading may be insufficient and uniform dispersibility may be insufficient. On the other hand, if L / D is too large, there is a tendency to cause decomposition due to shear heat generation due to excessive shearing or excessive retention.
  • the screw rotation speed is usually 10 to 400 rpm, preferably 30 to 300 rpm, more preferably 50 to 250 rpm. If it is too small, the discharge tends to become unstable, and if it is too large, the resin may deteriorate due to shearing heat generation.
  • the resin temperature at the time of melting in the extruder is usually 170 to 260 ° C, preferably 180 to 240 ° C, more preferably 190 to 235 ° C. If the composition temperature is too high, the reaction between the side chain 1,2-diol-containing PVA resin (A) and the polar functional group-containing fluororesin (B) may proceed excessively, resulting in gelation. On the other hand, when too low, melt-kneading will become inadequate and there exists a tendency for the dispersibility of polar functional group containing fluororesin (B) to become inadequate.
  • adjustment of a composition temperature can be normally performed by setting suitably the temperature of the cylinder in an extruder, and rotation speed.
  • the resin composition of the present invention obtained as described above can be melt-molded.
  • the shape of the composition is usually a shape such as pellets or powder. It is preferable to use a pellet shape from the viewpoint of small problems of charging into a molding machine, handling, and generation of fine powder.
  • a well-known method can be used for shaping
  • Cooling may be performed by bringing the PVA resin (A) into contact with a low-temperature organic solvent that does not dissolve the PVA resin (A), for example, an alcohol solvent, or by blowing cold air. Air cooling is preferable from the viewpoint of environment and safety.
  • the shape of the pellet is cylindrical or spherical, and the size and shape are not particularly limited.
  • the diameter is preferably 1 to 6 mm and the length is preferably 1 to 6 mm.
  • the diameter is preferably 1 to 5 mm.
  • minipellets having a diameter of 1 to 2 mm and a length of 1 to 2.5 mm are preferable in order to emulsify in water described later and efficiently emulsify.
  • the PVA-based resin composition having the above composition can be melt-molded, and the resulting molded product has excellent gas barrier properties and solvent resistance, and has improved bending fatigue resistance. Therefore, it can be used as various food and beverage packaging materials, containers, bag-in-box inner bags, container packings, pharmaceuticals, other chemicals, chemicals, organic liquid containers, and the like.
  • the surface free energy of the surface of the melt-molded product of the PVA resin composition of the present invention is smaller than the surface free energy of the melt-molded product of the side chain 1,2-diol-containing PVA resin alone. Therefore, in the case of a melt-molded product, particularly a film, adhesion between films can be suppressed. This means that the melt-formed film can be easily wound at room temperature and humidity, which is advantageous in industrial production.
  • the PVA-based resin composition of the present invention is based on excellent solvent resistance, is used for packaging materials that require severe solvent resistance, various battery members, surface protection layers for magnets made of rare metals, etc., for organic EL It can also be used as a sealing film.
  • the resin composition of the present invention can also be used as an emulsified dispersion in which a fluororesin is emulsified and dispersed.
  • the emulsified dispersion of the present invention is a liquid obtained by dispersing or dissolving the resin composition of the present invention with a liquid that can be uniformly mixed with the PVA resin or dissolves the PVA resin. Therefore, the emulsified dispersion of the present invention comprises a polyvinyl alcohol resin (A) containing a structural unit represented by the following formula (1); a fluororesin having a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond ( B); and a dispersion medium capable of dissolving or uniformly mixing the polyvinyl alcohol resin (A).
  • R 1 to R 6 each independently represents a hydrogen atom or an organic group, and X represents a single bond or a bonded chain.
  • the side chain 1,2-diol-containing PVA resin as the component A and the fluororesin as the component B used in the emulsified dispersion of the present invention can be the same compounds as those used in the resin composition. .
  • resin composition pellets in which the A component is a matrix and the B component is dispersed in the matrix are used.
  • the mixing ratio of component A and component B, component A: component B is 95: 5 to 55:45, preferably 90:10 to 60:40, and more preferably 85:
  • a resin composition pellet of 15 to 60:40, particularly preferably 80:20 to 65:35 is preferably used.
  • the dispersion medium can be uniformly mixed with the PVA resin, or the liquid that dissolves the PVA resin is specifically selected from the group consisting of water, a mixture of water and alcohol, and an amide solvent. At least one kind can be used.
  • the amide solvent N-methylpyrrolidone (NMP), dimethylformamide, dimethylacetamide, methylformamide and the like can be used.
  • water / alcohol mixture lower alcohols such as methanol, ethanol, isopropanol, and n-propyl alcohol are used as the alcohol.
  • the mixing ratio of water and alcohol is usually 100/0 to 40/60, preferably 90/10 to 50/50, more preferably 85/15 to 60/40. If there is too much alcohol, the emulsification dispersibility becomes insufficient, the storage stability of the emulsion is lowered, the viscosity of the emulsion is increased, and the handleability of the emulsion is lowered, which is not preferable.
  • the hydroxyl group of the side chain 1,2-diol-containing PVA resin (A), particularly the primary functional group and the polar functional group contained in the polar functional group-containing fluororesin (B) (preferably The product resulting from the reaction with the carboxyl group) or the formation of hydrogen bonds can act as a compatibilizing agent, and the fluororesin (B) is finely dispersed in the PVA resin (A) matrix. Therefore, when the resin composition of the present invention is mixed with a liquid capable of dissolving or uniformly mixing the PVA resin, that is, a dispersion medium, the side chain 1,2-diol-containing PVA resin constituting the sea part is obtained.
  • the polar functional group-containing fluororesin (B) constituting the island portion is contained in the hydroxyl group of the PVA resin (A), particularly the primary hydroxyl group and the fluororesin (B).
  • a product obtained by reaction with a polar functional group (preferably a carboxyl group or a carboxylic acid anhydride group) or formation of a hydrogen bond acts as a protective colloid agent to be dispersed in a dispersion medium.
  • a fluororesin cannot be dispersed alone in a dispersion medium such as water, a water / alcohol mixture, or an amide solvent, but the reaction product with the side chain 1,2-diol-containing PVA resin is a dispersoid. It is considered that a certain polar functional group-containing fluororesin (B) can be stably present by forming a spherical shape surrounding the protective resin colloid.
  • the emulsified dispersion of fluororesin can be prepared by putting pellets of the resin composition into a dispersion medium and stirring as necessary, preferably while heating.
  • the concentration of the resin composition of the present invention (solid content) with respect to the total amount of the emulsified dispersion is usually 1 to 50% by mass, preferably 3 to 45% by mass, more preferably 7 to 40% by mass.
  • solid content in this invention means the value measured by the drying loss method.
  • the concentration of the resin composition (solid content) with respect to the total amount of the emulsified dispersion is usually 10 to 50% by mass, preferably 20 to 45% by mass, more preferably 30 to 40% by mass. It is.
  • the concentration of the resin composition (solid content) of the present invention relative to the total amount of the emulsified dispersion is usually 1 to 50% by mass, preferably 3 to 20% by mass. %, More preferably 7 to 15% by mass.
  • the heating temperature is usually 20 to 80 ° C., preferably 40 to 70 ° C., and more preferably 50 to 68 ° C. Although it does not specifically limit, the higher temperature is preferable at the point which can shorten an emulsification dispersion
  • the stirring time is usually 0.5 to 10 hours, preferably 1 to 7 hours, more preferably 1 to 5 hours.
  • the fluororesin (including the protective colloid layer) as a dispersoid is usually a particle of usually about 100 to 800 nm, preferably 300 to 700 nm, more preferably about 400 to 600 nm.
  • the diameter is stably dispersed.
  • the above emulsified dispersion can be used for the production of the resin composition film. That is, when the emulsified dispersion is applied to a substrate and dried by heating, the dispersion medium volatilizes or evaporates, and a coating film having a side chain 1,2-diol-containing PVA resin as a matrix and a fluororesin as a domain is obtained. .
  • the drying temperature at this time is from room temperature to 150 ° C., preferably from 60 to 130 ° C., more preferably from 70 to 120 ° C.
  • the coating film formed from such an emulsified dispersion has excellent solvent resistance. Furthermore, it has very low swelling and insolubility with respect to ethylene carbonate, propylene carbonate, diethyl carbonate, dimethyl carbonate and the like used for the electrolyte solution of the Li ion secondary battery, and has durability against hydrogen fluoride and the like. Further, since it has sufficient heat resistance of 180 to 200 ° C. required for such a coating film, it is suitably used as a packaging material for Li ion secondary batteries, a surface treatment agent for electrodes and separators, and a binder for electrode active materials.
  • the binder of the present invention contains the above emulsified dispersion of the present invention. That is, the binder of the present invention comprises a side chain 1,2-diol-containing PVA resin (A); a fluororesin (B) having a polar functional group capable of reacting with a hydroxyl group or capable of forming a hydrogen bond; An emulsified dispersion containing a dispersion medium capable of dissolving or uniformly mixing the resin (A) is included. In particular, it is suitable as a binder for lithium ion secondary battery electrodes.
  • a fluorine-based polymer such as PVDF is widely used because of its excellent binding force with an active material. Furthermore, it is necessary to have a binding property that prevents the active material from being detached or peeled from the current collector even if it is bent or curved. From such a viewpoint, for example, Japanese Patent Application Laid-Open No. 2002-231251 proposes a binder in which a fluorine-based polymer and a conjugated diene-based polymer are dispersed in water.
  • the electrode binder also has better solvent resistance and has a binding force even when the current collector is bent or bent. There is a growing demand for binders that can be retained and that are excellent in stability of repeated charge and discharge.
  • the binder of the present invention can meet such a demand.
  • SBR styrene butadiene rubber
  • PVDF polyvinylidene difluoride
  • the binder of the present invention is useful as an aqueous binder that can be used for the positive electrode active material.
  • the binder of the present invention will be described taking a binder for a lithium ion secondary battery electrode as an example, but the binder of the present invention can also be applied to binder applications other than lithium ion secondary battery electrodes.
  • the binder for lithium ion secondary battery electrodes includes (A) a side chain 1,2-diol-containing PVA resin as a binder component, and (B) a polar functional group capable of reacting with a hydroxyl group or forming a hydrogen bond.
  • the fluororesin (B) is contained, and is usually prepared using the above emulsified dispersion of the present invention as a raw material.
  • the dispersion medium is also the solvent used in the above emulsified dispersion, that is, a solvent capable of dissolving or uniformly mixing the component A, specifically, water, a mixture of water and alcohol, and an amide solvent. At least one selected from the group consisting of can be used.
  • a solvent capable of dissolving or uniformly mixing the component A specifically, water, a mixture of water and alcohol, and an amide solvent.
  • the amide solvent for example, N-methylpyrrolidone (NMP), dimethylformamide, dimethylacetamide, methylformamide and the like can be used.
  • NMP N-methylpyrrolidone
  • dimethylformamide dimethylacetamide
  • methylformamide methylformamide
  • examples of the alcohol include lower alcohols such as methanol, ethanol, isopropanol, and n-propyl alcohol.
  • the amount of the binder resin component contained in the binder (the total content of component A and component B) is 1 to 60% by weight of the binder, preferably 5 to 50% by weight, particularly preferably 8 to 40% by weight. . Accordingly, the content of the emulsified dispersion of the present invention contained in the binder is an amount such that the content of the binder resin component falls within the above range, and may be appropriately set according to the solid content concentration of the emulsified dispersion.
  • the mixing ratio of the A component and the B component in the binder resin component is not particularly limited, but the mixing ratio (mass that allows the PVA resin to be a matrix and the fluororesin B component to be stably finely dispersed in the dispersion medium. Ratio).
  • the side chain 1,2-diol-containing PVA resin (A): fluororesin (B) 95: 5 to 55:45, preferably 90:10 to 60:40, more preferably 85:15. 60:40, particularly preferably 80:20 to 65:35.
  • the binder of the present invention includes a PVA resin other than the PVA resin containing a side chain 1,2-diol structural unit, other water-soluble polymers, etc., in order to adjust the viscosity of the binder. May be added as appropriate.
  • PVA resins other than the side chain 1,2-diol structural unit-containing PVA resins include unmodified PVA resins; carboxyl group-containing PVA resins; formalized PVA resins, butyral PVA resins, and the like.
  • water-soluble polymers other than PVA resins include cellulose derivatives such as methyl cellulose, ethyl cellulose, hydroxymethyl cellulose, hydroxypropyl methyl cellulose, hydroxybutyl methyl cellulose, hydroxyethyl cellulose, carboxymethyl cellulose, aminomethyl hydroxypropyl cellulose, aminoethyl hydroxypropyl cellulose, and the like.
  • Starch tragacanth, pectin, glue, alginic acid or salt thereof; gelatin; polyvinylpyrrolidone; polyacrylic acid or salt thereof polymethacrylic acid or salt thereof; acrylamides such as polyacrylamide or polymethacrylamide; vinyl acetate and maleic acid; Maleic anhydride, acrylic acid, acrylic acid, methacrylic acid, itaconic acid, fumaric acid, crotonic acid, etc.
  • Copolymer of saturated acid copolymer of styrene and the unsaturated acid
  • copolymer of vinyl ether and the unsaturated acid copolymer of vinyl ether and the unsaturated acid
  • salt or ester of the unsaturated acid and each copolymer, carrageenan examples thereof include polysaccharides such as xanthan gum. Among these, it is preferable to use cellulose derivatives.
  • the solid content in the binder that is, the ratio of the total solid content in the binder is usually 1 to 70% by mass, preferably 3 to 55% by mass, more preferably 5 to 50% by mass, and particularly preferably 8 to 40% by mass. This ratio is adjusted in consideration of the active material species and properties described later, and the viscosity when the slurry for an electrode is obtained.
  • the binder of the present invention can be produced by further adding other resin and dispersion medium to the emulsified dispersion as a raw material, if necessary, and mixing to obtain a predetermined concentration.
  • other resin and dispersion medium may be added, or a mixture of the resin composition pellets and other resin may be dissolved and dispersed in the dispersion medium. You may prepare by mixing an emulsified dispersion and the dispersion medium solution of other resin.
  • the binder having the above composition is excellent in heat resistance and solvent resistance based on the characteristics of the PVA resin as the binder resin component and the polar functional group-containing fluororesin by coating and drying.
  • a coating film excellent in electrochemical stability can be obtained. Therefore, when used as a binder between active materials or as an active material and a current collector, it can follow the expansion and contraction of the electrode active material due to repeated charge and discharge, and has excellent electrochemical stability. A quality electrode can be obtained.
  • the binder as described above is suitable as a binder for lithium ion secondary battery electrodes. It can be applied to both positive and negative electrodes.
  • Preparation of slurry for electrode, manufacture of electrode and lithium ion secondary battery (1) Preparation of electrode slurry and electrode production An electrode for a lithium ion secondary battery can be produced using a slurry liquid obtained by adding and mixing an active material and, if necessary, other components to the binder. .
  • the binder of the present invention tends to effectively obtain the effects of the present invention, particularly when a positive electrode active material is used, preferably when an olivine-type lithium metal phosphate is used.
  • a carbon material is preferable.
  • the carbon material include graphite-based carbon materials (graphite) such as natural graphite, artificial graphite, and expanded graphite, carbon black, activated carbon, carbon fiber, coke, soft carbon, and hard carbon. More preferably, graphite such as natural graphite, artificial graphite, and expanded graphite is used.
  • the average particle size of the active material is not particularly limited, but is preferably 1 to 100 ⁇ m, more preferably 1 to 50 ⁇ m, and further preferably 1 to 25 ⁇ m.
  • the value measured by the laser diffraction type particle size distribution measurement (laser diffraction scattering method) shall be employ
  • the content of the active material in the slurry is 10 to 95% by mass, 20 to 80% by mass, preferably 35 to 65% by mass.
  • the content ratio of the active material to the binder in the electrode slurry is usually 0.1 to 10 parts by mass, preferably 0.1 to 10 parts by mass in terms of solid content with respect to 100 parts by mass of the active material. To 5 parts by mass, particularly preferably 0.1 to 4. If the content of the electrode binder is too high, the internal resistance will increase. On the other hand, if the amount is too small, the desired binding force cannot be obtained, the electrode becomes unstable, and the charge / discharge cycle characteristics tend to deteriorate.
  • the electrode slurry may contain other materials in addition to the active material and the binder.
  • a conductive aid, an ion conductive polymer, and the like can be included.
  • the compounding ratio of these components is a known general range, and the compounding ratio can also be adjusted by appropriately referring to known knowledge about the lithium ion secondary battery.
  • “Conductive auxiliary agent” refers to a compound that is blended to improve conductivity.
  • the conductive aid include carbon powders such as graphite and acetylene black, and various carbon fibers such as vapor grown carbon fiber (VGCF).
  • VGCF vapor grown carbon fiber
  • the conductive assistant when a binder having a relatively low conductivity among the polymers is used, it is preferable to add a conductive assistant.
  • the blending amount of VGCF is preferably 1 to 10% by mass with respect to the total mass of the active material layer.
  • an electrode slurry may be prepared by adding a solvent for purposes such as viscosity adjustment and binder solid content adjustment.
  • a solvent for example, amide solvents such as N-methylpyrrolidone (NMP), dimethylformamide, dimethylacetamide, and methylformamide, and alcohol solvents such as methanol, ethanol, and higher alcohols can be used.
  • NMP N-methylpyrrolidone
  • dimethylformamide dimethylacetamide
  • methylformamide methylformamide
  • alcohol solvents such as methanol, ethanol, and higher alcohols
  • a stirrer for mixing the electrode binder, the active material, and the compounding agent and solvent used as necessary, a stirrer, a defoamer, a bead mill, a high-pressure homogenizer, or the like can be used.
  • the preparation of the electrode slurry is preferably performed under reduced pressure. Thereby, it can prevent that a bubble arises in the active material layer obtained.
  • An electrode can be produced by applying and drying the electrode slurry prepared as described above on a current collector. If necessary, it is preferable to increase the density by pressing after coating.
  • the current collector used for the negative electrode those used as the current collector for the negative electrode of the lithium ion secondary battery can be used. Specifically, since it is required to be an electrochemically inactive metal in a potential range where the negative electrode (carbon electrode) functions, a metal foil such as copper or nickel, an etching metal foil, an expanded metal, or the like is used. .
  • the current collector used for the positive electrode include metal materials such as aluminum, copper, nickel, tantalum, stainless steel, and titanium. The current collector can be appropriately selected and used depending on the type of the target power storage device.
  • An electrode layer can be formed by applying and drying an electrode slurry on each current collector.
  • Examples of the method for applying the electrode slurry to the current collector include a doctor blade method, a reverse roll method, a comma bar method, a gravure method, and an air knife method.
  • the treatment temperature is usually 20 to 250 ° C., more preferably 50 to 150 ° C.
  • the treatment time is usually 1 to 120 minutes, and more preferably 5 to 60 minutes.
  • the thickness of the active material layer (the thickness of one surface of the coating layer) is usually 20 to 500 ⁇ m, more preferably 20 to 300 ⁇ m, and still more preferably 20 to 150 ⁇ m.
  • Lithium ion secondary battery The lithium ion secondary battery provided with the electrode produced as mentioned above is demonstrated.
  • the binder of the present invention may be used as the binder of the active material.
  • an aprotic polar solvent that dissolves a lithium salt is used.
  • low-chain solvents such as dimethyl carbonate, ethyl methyl carbonate, and diethyl carbonate, which are low-viscosity solvents, are contained in cyclic carbonate high dielectric constant / high boiling point solvents such as ethylene carbonate and propylene carbonate. Used.
  • allyl ethyl carbonate vinyl ethylene carbonate, vinylene carbonate, maleic anhydride, 2-vinyl pyridine, vinyl acetate, etc. assists the formation of a solid electrolyte interface (SEI) and provides irreversible capacity. It is preferable at the point to reduce.
  • SEI solid electrolyte interface
  • lithium salt of the electrolyte examples include inorganic salts such as LiClO 4 , LiPF 6 , LiBF 4 , LiAsF 6 , LiCl, LiBr, LiCF 3 SO 3 , LiN (SO 2 CF 3 )) 2 , LiN (SO 2 C 2 F 2 5 ) 2 , organic compounds such as LiC (SO 2 CF 3 ) 3 , LiBC 4 O 8, etc., which are commonly used as electrolytes for non-aqueous electrolytes may be used.
  • LiPF 6 , LiBF 4 or LiClO 4 is preferably used.
  • the separator is not particularly limited, and a polyolefin nonwoven fabric or a porous film can be used.
  • the structure of the secondary battery is not particularly limited, and can be applied to any conventionally known form / structure such as a stacked (flat) battery or a wound (cylindrical) battery.
  • the electrical connection form (electrode structure) in the lithium ion secondary battery can be applied to both (internal parallel connection type) batteries and bipolar (internal series connection type) batteries.
  • Emulsification / dispersibility in water 20 parts of pellets of the resin composition were put into 80 parts of water at ordinary temperature, immersed in a container containing warm water at 80 ° C. and stirred for 90 minutes. O: A good emulsified dispersion was obtained. X: A precipitate was formed or completely dissolved.
  • Electrochemical stability Using a V-4C voltammetry cell manufactured by BAES Co., Ltd., the change in response current when the electrode potential was swept was measured.
  • the prepared electrode is a working electrode (electrode area 0.25 cm 2 ), a counter electrode is a platinum electrode, a reference electrode is a silver electrode (Ag / Ag + : AgSO 3 CF 3 ), and an electrolyte is ethylene carbonate (EC) / ethyl.
  • EMC methyl carbonate
  • the electrode potential was swept at a potential sweep rate of 5 mV / sec and a potential sweep range of ⁇ 0.5 to 2.4 V (reference electrode). The response current was measured. The measurement was performed at a temperature of 25 ° C. for 5 cycles.
  • a methanol solution of the polymer was used.
  • the methanol solution was further diluted with methanol, adjusted to a concentration of 45%, charged into a kneader, and while maintaining the solution temperature at 35 ° C., a 2% methanol solution of sodium hydroxide was added to vinyl acetate in the copolymer.
  • Saponification was performed by adding 11.5 mmol with respect to 1 mol of the total amount of structural units and 3,4-diacetoxy-1-butene structural units. As saponification progressed, the saponified product precipitated and became particulate when it was filtered.
  • the obtained saponification product was thoroughly washed with methanol and dried with a hot air dryer to obtain a PVA resin (A1) having a side chain 1,2-diol structural unit of the above formula (1a).
  • the degree of saponification of the obtained side chain 1,2-diol-containing PVA resin (A1) was analyzed by the alkali consumption required for hydrolysis of residual vinyl acetate and 3,4-diacetoxy-1-butene. It was 99.9 mol%. The average degree of polymerization was 450 when analyzed according to JIS K6726.
  • the content of the 1,2-diol structural unit represented by the formula (1a) is an integral measured by 1 H-NMR (300 MHz proton NMR, d6-DMSO solution, internal standard substance: tetramethylsilane, 50 ° C.). It was 6 mol% when computed from the value.
  • the MFR 210 ° C., load 2160 g
  • the melt viscosity (220 ° C., shear rate 122 sec ⁇ 1 ) was 1148 Pa ⁇ s.
  • Polar functional group-containing fluororesin modified fluororesin
  • B1 A polymerization tank equipped with a stirrer having an internal volume of 430 liters was degassed, and 200.7 kg of 1-hydrotridecafluorohexane and 1,3-dichloro-1,1,2,2,3-pentafluoropropane ( AK225cb manufactured by Asahi Glass Co., Ltd., hereinafter referred to as “AK225cb”.) 55.8 kg was charged, and 1.3 kg of CH 2 ⁇ CH (CF 2 ) 4 F was further charged as a polymerization monomer.
  • AK225cb 1-hydrotridecafluorohexane and 1,3-dichloro-1,1,2,2,3-pentafluoropropane
  • the solvent was distilled off from the resulting slurry to obtain a fluororesin having an acid anhydride group as a polar functional group, and this was vacuum dried at 130 ° C. for 4 hours, whereby 30 kg of an acid anhydride group-containing fluororesin ( B1) was obtained.
  • the crystallization temperature of the acid anhydride group-containing fluororesin (B1) is 175 ° C.
  • the Q value is 12 mm 3 / sec
  • the obtained resin composition pellets were formed into a film with a thickness of 30 ⁇ m using a twin-screw extruder (Technobel) under the following conditions.
  • Screen mesh 90/90 mesh Screw rotation speed: 200 rpm
  • Discharge rate 1.5kg / hr Die: width 300mm
  • Reference Example Table 1 shows the results of measurement and evaluation in the same manner for the side chain 1,2-diol-containing PVA resin alone as a reference example.
  • fluororesin polytetrafluoroethylene
  • A1 side chain 1,2-diol-containing PVA resin
  • the resin composition containing the thermoplastic elastomer component greatly improves the bending fatigue resistance, which has been a problem in the side chain 1,2-diol-containing PVA resin (reference example). I was able to improve. However, as is apparent from FIG. 2, the domain was eluted in any solvent of styrene and xylene, and the solvent resistance could not be satisfied. In addition, an emulsion dispersion of a thermoplastic elastomer could not be prepared.
  • the bending fatigue resistance of the side chain 1,2-diol-containing PVA resin is improved, and the side chain 1 , 2-diol-containing PVA resin inherently had solvent resistance.
  • An emulsified dispersion could also be prepared.
  • the surface free energy of the melt-formed film was smaller than that in the case of the side chain 1,2-diol-containing PVA resin film alone (reference example). Therefore, adsorption of substances on the film surface, adsorption between films during winding, and the like are less likely to occur.
  • Example 4 The resin composition pellets of Example 2 prepared above were dissolved in water to prepare a 20% by mass emulsion dispersion. 5.0 parts of this emulsified dispersion, 0.5 parts of a 2% by weight aqueous solution of carboxymethylcellulose (Nippon Paper Chemicals F20LC) as a thickener, 2.0 parts of acetylene black as a conductive additive are blended, and water 6.6 is further added. Parts were blended and mixed with a planetary mixing stirrer to obtain a slurry for measurement.
  • the binder composition used for the slurry contains a binder resin component, a thickener, and a dispersion medium at a mass ratio shown in Table 2.
  • the obtained slurry for measurement was applied onto an aluminum foil having a thickness of 20 ⁇ m using an applicator (clearance 170 ⁇ m). After coating, the temperature was maintained at 80 ° C. for 10 minutes, and then the temperature was raised to 105 ° C. over 25 minutes, followed by drying at 105 ° C. for 10 minutes. After drying, it was compressed with a roll press (clearance 12 ⁇ m) and dried under reduced pressure at 130 ° C. for 24 hours to obtain a working electrode. The electrochemical stability was evaluated based on the above evaluation method using the working electrode thus prepared. The obtained cyclic voltammogram is shown in FIG. 3, and the evaluation results are shown in Table 2.
  • Comparative Example 2 Polyvinylidene fluoride was used as the binder resin component.
  • An N-methylpyrrolidone solution of polyvinylidene fluoride (8% by mass) (# 1100 manufactured by Kishida Chemical Co., Ltd.) was used as a binder.
  • acetylene black was added and mixed as a conductive additive to prepare a working electrode slurry. Using this slurry, a working electrode was prepared and evaluated in the same manner as in Example 4.
  • FIG. 4 shows the obtained cyclic voltammogram, and Table 2 shows the evaluation results.
  • Comparative Example 3 Styrene butadiene rubber was used as a binder resin component.
  • a binder containing an aqueous dispersion of styrene-butadiene rubber (48.4% by mass) and the thickener used in Example 4 (2% by mass aqueous solution of carboxymethyl cellulose) in the proportions shown in Table 2 was used.
  • Acetylene black as a conductive additive was added and mixed, and a working electrode slurry was prepared in the same manner as in Example 4. Using this slurry, a working electrode was prepared and evaluated in the same manner as in Example 4. The obtained cyclic voltammogram is shown in FIG.
  • the first cycle of the binder using styrene butadiene rubber (Comparative Example 3) showed a large current value of 2.5 mA / cm 2 , but the current decreased from around 1.5 V, and then the current value remained low. From this, it can be seen that the film peeled off. Actually, when the state of the electrode was visually observed after the fifth cycle measurement, it was confirmed that the coating film was peeled off. It is presumed that the styrene butadiene rubber as a binder component was oxidized and deteriorated at a voltage of 1.5 V or more.
  • binders whose binder components are PVDF (Comparative Example 2) and styrene butadiene rubber (Comparative Example 3) are insufficient as binders for electrodes. That is, the binder whose binder component is PVDF (Comparative Example 2) or styrene butadiene rubber (Comparative Example 3) does not have sufficient binder power, and the resulting coating film is easily oxidized and deteriorated by high voltage. Therefore, the electrochemical stability is low. Furthermore, it is thought that this is because the flexibility to follow the repeated expansion and contraction associated with the redox of the electrode was insufficient.
  • the current value increases with repeated charge and discharge.
  • the increasing tendency of the response current with increasing potential was stable.
  • the state of the electrode was visually confirmed after completion of the measurement in the fifth cycle, no peeling off of the coating film was observed.
  • the current value was high, and no spike current was observed. Therefore, it is presumed that there was no peeling of the coating film that could not be visually confirmed. Therefore, the binder of this invention is excellent in the binder force with respect to a collector.
  • the coating film is excellent in electrochemical stability because it does not undergo oxidative degradation even under high voltage and has resistance to the electrolytic solution. Moreover, it has the flexibility which can follow the expansion
  • the resin composition of the present invention is improved in the bending fatigue resistance of the PVA-based resin, retains the gas barrier property and solvent resistance, which are the advantages inherent in the PVA-based resin, and can be melt-molded. It can be suitably used as a packaging material for various foods and beverages, chemicals, chemicals, packaging containers, and the like. Further, since the surface free energy is small, it is industrially useful that the film formed by the melting method can be easily wound at room temperature and normal humidity.
  • an emulsified dispersion in which the polar functional group-containing fluororesin is uniformly dispersed can be obtained, so that it can be used as a binder.
  • a binder can form a coating film excellent in solvent resistance, and has flexibility to follow the repeated expansion and contraction associated with oxidation / reduction of the electrode, and is excellent in electrochemical stability. It can be suitably used as a binder for repeated lithium ion secondary battery electrodes.

Abstract

Cette invention concerne une composition de résine qui contient une résine à base de PVA (A) contenant un 1,2-diol à chaîne latérale pouvant être moulée à chaud, et une résine fluorée (B) ayant un groupe fonctionnel polaire qui est soit capable de réagir avec les groupes hydroxyle, soit capable de former une liaison hydrogène. Le composant (A) et le composant (B) ont une excellente affinité, et par conséquent si l'un ou l'autre du composant (A) ou du composant (B) est utilisé comme matrice, l'autre peut être finement dispersé dans la matrice, pour obtenir une composition de résine ayant d'excellentes propriétés de barrière aux gaz, ainsi qu'une excellente résistance aux solvants, et une excellente résistance à la rupture par fatigue en flexion. Cette invention concerne également une suspension émulsifiée et un liant utilisant ladite composition de résine.
PCT/JP2013/062325 2012-04-27 2013-04-26 Composition de résine et son utilisation WO2013161975A1 (fr)

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JP2015144124A (ja) * 2013-12-27 2015-08-06 日本合成化学工業株式会社 リチウムイオン二次電池電極用バインダー組成物、リチウムイオン二次電池電極、及びリチウムイオン二次電池
JP2016066601A (ja) * 2014-09-22 2016-04-28 日本合成化学工業株式会社 リチウムイオン二次電池電極用バインダー組成物、リチウムイオン二次電池電極、及びリチウムイオン二次電池
US20180016430A1 (en) * 2014-12-27 2018-01-18 The Nippon Synthetic Chemical Industry Co., Ltd. Saponified ethylene-vinyl ester copolymer resin composition, resin tube for high-pressure gas or resin liner for composite container, and high-pressure gas hose or composite container
JP2018018728A (ja) * 2016-07-28 2018-02-01 日本合成化学工業株式会社 リチウムイオン二次電池正極用バインダー組成物、リチウムイオン二次電池正極、及びリチウムイオン二次電池
JP2018060603A (ja) * 2016-09-30 2018-04-12 日本合成化学工業株式会社 リチウムイオン二次電池正極用バインダー組成物、リチウムイオン二次電池正極、及びリチウムイオン二次電池
WO2019031521A1 (fr) * 2017-08-09 2019-02-14 Ａｇｃ株式会社 Composition de copolymère contenant du fluor
JPWO2019031521A1 (ja) * 2017-08-09 2020-09-24 Ａｇｃ株式会社 含フッ素共重合体組成物
JP7136105B2 (ja) 2017-08-09 2022-09-13 Ａｇｃ株式会社 含フッ素共重合体組成物

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US9487650B2 (en) 2016-11-08
CN104245829A (zh) 2014-12-24
EP2842998A4 (fr) 2015-12-23
JP6143531B2 (ja) 2017-06-07
JP2013241587A (ja) 2013-12-05
EP2842998A1 (fr) 2015-03-04
US20150038633A1 (en) 2015-02-05
EP2842998B1 (fr) 2017-03-08

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